CO-COMPOSTING PROCESS AND APPARATUS FOR TREATING SOLID WASTE AND SEWAGE SLUDGE

Abstract: The present application describes methods and apparatus for co-processing solid organic waste material and sludge to form a material suitable for agricultural application. The method comprises the steps of forming an admixture of solid organic waste materials and sludge in one or more containment vessels (12, 14, 16 and 18). At least one of the vessels has means for mixing (118 and 122) the admixture formed, and is further equipped with means for placing gases and water into the vessel (30) and removing gases and water from the vessel (32). The vessel is equipped with temperature controls (222) to facilitate imposition of various growth conditions within the vessel. The vessel further comprises opening means for receiving solid organic waste material and sludge and discharging one or more biodegradable products. The mixing apparatus maintains the admixture in contact with gases and water and provides temperature uniformity within the vessel.

Description: CO-COMPOSTING PROCESS AND APPARATUS FOR TREATING SOLID WASTE AND SEWAGE SLUDGE This application is a Continuation-in-Part of U.S. Serial No, 08/077,238, filed June 14, 1993 and U.S. Serial No. 08/251,515 filed June 6, 1994, entitled: Co-Composting Process and Apparatus for Treating Solid Waste and Sewage Sludge. The present invention relates to processes and apparatus for rendering solid organic waste and sludge into organic material suitable for application to soil. Background of the Invention This invention relates to the co-processing of solid organic waste material such as agricultural, industrial or municipal organic solid waste, with sludge. Sludge may also be derived from agricultural, industrial or municipal sources. As used in this application, the term "solid organic waste material" refers to refuse of the type generated by homeowners/apartment dwellers, businesses and industry. This refuse encompasses municipal solid waste which typically has the composition set forth in Table 1. TABLE 1 Paper and Cardboard 40% Glass 8% Assorted Metals 6% Yard and Food Waste 17% Plastic 12% Assorted Fabrics 13% The materials and percentages set forth in Table 1 may deviate with geographical area and the socioeconomic conditions of the community from which it is derived. Approximately 70% of the refuse identified in Table 1 is biodegradable. The term "sludge is used to denote a cell type sludge of the type generated in secondary biological treatment processes of waste materials, Cell type sludge is characterized by a community of microbes often comprising Zoogloea ra iga. This organism synthesizes and secretes a polysaccharide gel. The gel allows the microbe community to agglomerate in floes. Waste treatment processes generate sludge, which sludge, although often recycled and aerobically digested, must be disposed of at some point. The microbial community no longer has the activity desired or, the processes have generated sludge in excess of the handling capacity of the system. The sludge generated is generally rich in nitrogen which makes the material attractive for use as a fertilizer. However, the material has a high water contact that is difficult to remove. Toxic metals tend to accumulate in sludge, which toxic metals are also difficult to remove. Summary of the Invention The present invention is directed methods and apparatus for co-processing solid organic waste material, such as agricultural, industrial or municipal organic solid waste with sludge. One embodiment of the present invention features a method of making an organic material- from solid organic waste material and sludge. The method comprises the steps of forming an admixture of a solid organic waste material and sludge in one or more containment vessels, At least one of the vessels has means for mixing the admixture formed, and is further equipped with means for placing gases and water into the vessel and removing gases and water from the vessel. The vessel is equipped with temperature controls to facilitate imposition of various growth conditions within the vessel. The vessel further comprises opening means for receiving solid organic waste material and sludge and discharging one or more biodegradable products, The mixing apparatus maintains the admixture in contact with gases and water and provides temperature uniformity within the vessel. The gas input, water input and temperature control facilitate imposing one or more growth conditions within the vessel, The method further comprises imposing first growth conditions on the admixture. The first growth conditions comprise a temperature of 165° to 200°F, gaseous water concentration of gases within the vessel of 25-40%, and an oxygen gas concentration to promote the growth of thermophilic microorganisms in the admixture. The thermophilic microorganisms biodegrade the admixture to form a thermophilic biodegradation product. In the event the thermophilic biodegradation product does not comprise sufficient mesophilic microorganisms, the method further comprises the step of forming a second admixture of a mesophilic microorganism and the thermophilic biodegradation product. The method further comprises imposing second growth conditions on the second admixture or said thermophilic biodegradation product which second growth conditions comprise a temperature of 145-164°F, gaseous water concentration within the vessel of 25-45%, and an oxygen concentration sufficient to promote the growth of one or more mesophilic microorganism. The mesophilic microorganisms biodegrade the thermophilic biodegradation product to form a mesophilic biodegradation product comprising an organic material , This organic material may be suitable for some agricultural applications; however, most preferably, the mesophilic biodegradation product is further processed by performing an additional step, in the event the mesophilic biodegradation product does not comprise sufficient microorganisms of a third microorganism group, forming a third admixture comprising the mesophilic biodegradation product and a third microorganism group. The third microorganism group comprises actinomycetes , The method further comprises the step of imposing third growth conditions on the third admixture or the mesophilic biodegradation product. The third growth conditions comprise a temperature of 110-144°F, gaseous water concentration within the vessel of 25-45%, and sufficient oxygen gas concentra ion to promote the growth of said one or more organisms of the third microorganism group, The third microorganism group biodegrades the mesophilic biodegradation product to form an organic product. Preferably, the third microorganism group further comprises protozoa and fungi. The biodegradation product of the third admixture is preferably a compost suitable for typical agricultural applications. The term "compost" is sometime used to refer to decaying or decayed organic material derived from leaves from plants. As used herein, the term "compost" refers to a particular mixture of organic material, rich in nitrogen, without reference to the origin, but with features typically associated with compost products suitable for fertilizers. As used herein, the term "does not comprise sufficient thermophilic, mesophilic or microorganisms of a third group," refers to an amount of microorganisms to accomplish a process step in a desired period of time. Normally, the period of time is 24 to 48 hours. The process step requirements for such period of time are determined by the number of microorganisms in the admixture or product and the amount of admixture and product to be processed. Typically, organic waste material and sludge has pathogenic organisms. The present method features first growth conditions which are incompatible with the pathogens. The pathogens are destroyed by the elevated temperatures to form a thermophilic biodegradation product with a reduced pathogen load. Preferred first growth conditions comprise a temperature range of 175°-178°F. Preferably, the water content of the air is maintained at approximately 33% by volume. Preferably, the second growth conditions comprise a temperature of between 145°F and 162° and a water content of 30% by volume of gas. Preferably, the third growth conditions comprise a temperature range between 120°F and 144°F. Preferably, the water content of the gases within the vessel is reduced to 27% by volume. The temperature and the oxygen and water concentration of the gases within the vessel are maintained by a flow of gases through the vessel through the gas inlet and gas outlet means. By way of example, the temperature can be controlled by reducing the flow of gases to produce higher temperatures wherein the microorganisms have sufficient oxygen to maintain growth at the lower rate of gas flow. The flow of gases can be increased to reduce the temperature. However, where gases are used to reduce the temperature, preferably the gases are substantially inert to the biological process. An increased flow of oxygen may actually increase the rate of biological processes within the vessel and contribute to an elevated temperature. However, where the gas in an inert gas, the gas serves to vent heat process and does not contribute to further metabolic processes. A preferred inert gas is carbon dioxide, which is the by-product of the metabolic processes taking place in the vessel. Similarly, where an elevated temperature is desired, the present invention features the addition of additional oxygen to promote growth by the microorganisms. Preferably, the gases are mixed in a plenum in fluid communication with the vessel inlet. These gases can include gaseous water or, in the alternative, water can be added to the vessel in a sufficient liquid quantity to form the water vapor content desired. Preferably, the outlet of the vessel, for the removal of gases, is in communication with a scrubber to remove noxious odors. Noxious odors are typically generated only within the first two to four hours of the thermophilic growth conditions. Preferably, thermophilic organisms are present in the sludge. The imposition of thermophilic growth conditions causes a rapid proliferation of such thermophilic organisms. Mesophilic organisms and microorganisms of the third microorganism group may be present in the first thermophilic biodegradation product carried over from the sludge or solid organic waste material. Upon imposition of mesophilic growth conditions, such organisms proliferate to form a mesophilic biodegradation product. In the event that insufficient mesophilic microorganisms survive the thermophilic growth conditions, one embodiment of the present invention features the addition of mesophilic microorganisms to initiate mesophilic growth within the vessel and the addition of the third microorganism group to initiate growth under the third growth conditions. Thermophilic organisms may also be added to the sludge and solid organic waste material admixture if a particular thermophilic organism is desired for the process. Mesophilic microorganisms preferably comprise Bacillus subtillis. However, other microorganisms may be part of the culture. Mesophilic microorganisms are preferably selected from similar processes undergoing mesophilic growth conditions to produce a mixed culture in which the microorganisms have similar growth profiles. The growth profiles should be such that the microorganism substantially complete their rapid growth stage within the typical admixture which receives such mesophilic microorganisms. Indeed, cultures obtained from the second growth conditions, which favor mesophilic microorganisms, can be saved and grown for further use. The third microorganism group are preferably actinomycetes, protozoa and fungi, However, other microorganisms may be part of the culture. Such microorganisms are also preferably selected for similar growth and may be obtained from ongoing processes undergoing third growth conditions and saved and grown for further use. Preferred microorganisms comprise Proteus vulgaris, Streptococcus pyoqenes, Gladosporum herbarum, Cyanobacteria, Azotobacter, Bacillus subtilis, Bacillus mesenterious, Escherichia coli, Saccharomyces, cerevisiae, Actinomycetes, Fungi, Protozoa, Algae and Myxobacteria. One embodiment of the present method features a rotable cylindrical vessel having one or more baffles. The baffles have planar surfaces extending inward from the cylindrical wall into the chamber for imparting direction and movement to solids and liquids to facilitate mixing, Preferably the baffles are rotatable to assume at least two of four positions. The four positions comprise a first inclined position with respect to the vessel rotation such that the planar surfaces move solids and liquids in a first direction. One of the positions comprises a second inclined position with respect to the vessel rotation wherein the planar surfaces move solids and liquids in a second direction opposite the first direction. A further position comprises a third position wherein the planar surfaces are perpendicular to the vessel rotation to maintain the solids in an area of the vessel while subjecting the solids and liquids to mixing. A fourth position comprises a position wherein the planar surfaces are in the plane defined by the rotation of the vessel, to allow rotation of the vessel with minimal mixing. Preferably, each baffle comprises a planar surface affixed to a rotatable shaft mounted to the cylindrical wall of the vessel. Preferably, the vessel has a plurality of baffles which baffles assume one of the four positions in cooperation to provide movement of solids and liquids throughout the vessel. Thus, each baffle assumes one of the inclined positions, to form an auger like spiral along the inside of the cylindrical wall of the vessel. This auger like spiral moves solids and liquids throughout the vessel as the vessel rotates to facilitate loading and unloading of material. The baffles are also able to assume a perpendicular position to promote mixing of the solids and liquids. If rotation of the vessel is desired without substantial mixing, the baffles are capable of assuming a neutral position wherein the planar surface is oriented with the plane of rotation of the vessel. Preferably, the baffles are able to assume three of the four positions. The position in which the baffles are perpendicular to the rotation exerts substantial loads or means holding the baffles to the wall and is not a preferred position. Preferably, the vessel further comprises shredding means for tearing solids as the vessel is rotated. These shredding means preferably comprise inwardly projecting spikes or protrusions which grab and tear packing materials and other materials that are capable of being reduced in size. Preferably, the vessel is an elongated cylinder with two ends, one of the ends having a first opening for receiving solid organic waste material. The opposite end has a second opening for discharging one or more organic products. Movement of such solid organic waste material and organic products is facilitated by the rotation of the vessel and the baffles. Preferably the vessel has sensors for monitoring conditions for microorganism growth. These conditions include temperature and water, carbon dioxide methane and oxygen sensors. Such sensors are preferably in communication with computer monitoring means which may comprise further control means for adjusting the input of gases, water and the control of temperature. A further embodiment of the present invention features an apparatus for processing solid organic waste material and sludge. The apparatus comprises a vessel having a cylindrical wall having an axis of rotation and two opposing end walls. The cylindrical wall and end walls define a chamber. The vessel has openings means, mixing means, gas input means, water input means, temperature control means, and gas output means. The opening means comprise one or more openings for receiving solid organic waste material and, discharging one or more biodegradation products. Mixing means are provided for forming an admixture of a solid organic waste material and sludge, and for forming an admixture of one or more biodegradation products and microorganisms. Mixing means further mixes the admixtures formed within the chamber, brings such admixtures in contact with gases and water, and provides temperature uniformity throughout the vessel . The mixing means preferably cooperates with the rotation of the vessel to distribute solids and liquids throughout the vessel upon receiving solids and liquids within the chamber from the opening means. The mixing means preferably cooperates with the rotation of the vessel to propel the solids to the opening means to discharge the solids from the vessel. The gas input means, water input means and temperature control means impose one or more growth conditions within the vessels and operate in cooperation with gas output means for discharging gases from the vessel. The apparatus further comprises a scrubber in communication with the gas outlet means for receiving gases from the vessel and for removing noxious gases . The scrubber is vented to discharge process gases to the atmosphere. The apparatus further comprises vessel rotating means for rotating the vessel about the axis of rotation and in cooperation with mixing means to direct movement of the solids and liquids within the vessel. The vessel receives solid organic waste material and sludge within the chamber and forms an admixture by rotating the vessel. First growth conditions are imposed during the rotation of the vessel which growth conditions comprise a temperature of 165-200°F, gaseous water in a concentration of 25-40% and sufficient oxygen to promote the growth of thermophilic microorganisms. The thermophilic microorganisms biodegrade the admixture to form a thermophilic biodegradation product. In the event mesophilic microorganisms are not present in the thermophilic biodegradation product, the vessel further receives a mesophilic micro-organism through said opening means and a second admixture is formed with said mixing means. The second admixture comprises a thermophilic biodegradation product and the mesophilic microorganism. The vessel imposes second growth conditions on the second admixture or the thermophilic biodegration product to promote the growth of the mesophilic microorganisms. The second growth conditions comprise a temperature of 145-164°F, gaseous water within the chamber of 25-45%, and sufficient oxygen to support of mesophilic microorganisms. The mesophilic microorganisms form a mesophilic biodegradation product comprising an organic material, which is discharged from the chamber. Preferably, prior to discharge, in the event a third microorganism group is not present in the mesophilic biodegradation product, the vessel receives a third microorganism group comprising actinomycetes. The mixing means cooperates with the rotating vessel to form a third admixture comprising the third microorganism group and the mesophilic biodegradation product. The vessel imposes third growth conditions on the third admixture or the mesophilic biodegradation product, which third growth conditions comprise a temperature of 110-144°F, gaseous water concentration of 25-45% and sufficient oxygen to support the growth of one or more actinomycetes for forming a third biodegradation product comprising an organic material. Preferably, the vessel comprises sensors for one or more of the following compositions including carbon dioxide, water, methane, and oxygen and one or more sensors for temperature. Preferably the sensors are in communication with computer control means for regulating gas input means, water input means and temperature control means. Preferably, the apparatus further comprises mixing means comprising one or more baffles projecting inwardly into the chamber from the cylinder wall. The baffles have a planar surface for imparting movement and direction into solids and liquids upon rotation of the vessel. The one or more baffles are capable of assuming at least two or four positions. One of the positions comprises the planar surface inclined with respect to the direction of rotation of the vessel to impart movement of solids and liquids in a first direction upon rotation of the vessel in a first rotational direction. One of the positions comprising the second planar surface inclined in the opposite direction for directing solids and liquids in a second direction opposite the first direction upon rotation of the vessel in the first rotational direction. One of the positions comprising the planar surface perpendicular to the access of rotation to mix solids and liquids without imparting movement of solids and liquids to one of the ends, for mixing the solids and liquids. And, one of the positions comprising the planar surface in a plane defined by the arc of rotation of the vessel which position does not provide substantial mixing. Preferably, the baffles are able to assume three of the four positions. The perpendicular orientation of baffles places substantial loads on the means for holding baffles to the vessel wall and is not a preferred position. Preferably, the vessel is supported by rollers in communication with power means including DC electric motors. Preferably, the rollers are held within tracks on the vessel for maintaining the position of the vessel on the rollers. The present invention features the process of co-composting solid organic waste material with sludge in an aerobic process using mixed populations of microorganisms under rigorous biological controls. The resulting composition is compost-like, stable, substantially free of offending odors, and pathogenic bacteria. Metal toxicants which accumulate in sludge are diluted with solid organic waste material allowing the finished product to be used as an agricultural compost. The co-composting process of the present invention is performed in a continuous three to five day period within a single vessel. This single vessel is processed through three growth conditions. Preferably, the mesophilic microorganisms are used in cooperation with enzymes disclosed in Italian patent number 999,818 and in Spanish patent number 435,460, the disclosure of each of such patents is herewith incorporated by reference. Embodiments of the present invention feature in vessel processing. Such in vessel processing eliminates rodents, flies and odors. Embodiments of the present invention reduce solid organic waste material by 75% and process sludge completely into a useful end product. Features of the present invention are well suited for fixed facilities in which approximately 250 tons per day are processed per vessel. However, the present invention further is amenable to a number of different sizes and scales. The present invention can be mounted on a mobile trailer bed or rail car to allow the process to be taken to agricultural, industrial, or municipal sites or other sites where the utility of the methods and apparatus can be utilized. Similarly, the entire apparatus can be placed aboard a water vessel such as a barge or ship. In such manner, a plurality of communities can utilize the features of a single apparatus of the present invention. Other features of the present invention will become apparent from the following detailed description in connection with the accompanying drawings which follow. Brief Description of the Drawings FIG. 1 depicts a plan view of the apparatus for carrying out the process of the invention embodying features of the present invention; FIG. 2 depicts a vessel and a ram operated hopper embodying features of the present invention; FIG. 2A depicts an enlarged view of the leading edge of the sliding bottom of the hopper; FIG. 3 depicts, in a partial cut away, a perspective view of a vessel embodying features of the invention; FIG. 4 depicts a section view of the vessel along line 4-4 of FIG. 2; FIG. 5 depicts an end view of a variable pitch baffle; FIG. 6 depicts a side view of the nozzle injector for fluids to be injected into the digester apparatus; FIG. 7 depicts a section view of the nozzle injector along line 7-7 of FIG. 6; and FIG. 8 depicts a plan view of the control system for the invention. Detailed Description of Preferred Embodiments The present apparatus and process will be described in detail with respect to drawings which depict a fixed processing plant for receiving solid organic waste material and sludge. However, the process and apparatus can be changed to different scales and sizes, Other embodiments of the present invention feature an apparatus mounted to a trailer bed, suitable for transportation on highways, or mounted on a rail car, suitable for transportation on railroads, or on water transport vessels for transportation on oceans and waterways. Turning now to Fig. 1, a fixed processing plant generally designated by the numeral 10, is illustrated. The plant 10 has the following major elements: vessels 12, 14, 16 and 18; MSW handling area 20, finished product conveying means 22, sludge storage means 24, sludge conveying lines 26, scrubber 28, input conduits 30, output conduit 32, and vessel rotation means 34. Each vessel 12, 14, 16 and 18 has similar features which will be described with respect to vessel 12, for purposes of clarity. Vessel 12 has a cylindrical wall 36 and two ends 38a and 38b. One of the ends 38a has an opening to be described later, for receiving MSW and one of the ends 38b has an opening to be described later for discharging finished product. Vessel 12 is capable of rotation about an axis of rotation with respect to cylindrical wall 36. Turning briefly now to Figs. 1 and 2, vessel 12 is supported on powered rollers 34. Power rollers 34 are coupled to direct current electric motors to rotate vessel 12 at a rate of up to 20 to 30 revolutions per hour. Preferably, vessel 12 has a track 40, comprising an indentation in the outer cylindrical wall 36, as best seen in Fig. 2. Track 40 maintains the position of vessel 12 as it rotates on power rollers 34. It will be readily recognized that not all power rollers 34 must be coupled to motors, Only one roller must be coupled to a motor and all others may be idler rollers. Preferably, rollers 34a and b towards the ends of 38a and 38b of vessel 12 are coupled to motors. Middle rollers 34c are idler rollers, which are not coupled to motors. Returning now to Fig. 1, vessels 12, 14, 16, and 18 communicate with the MSW handling area 20 by means of a hopper assembly 46a, b, c, and d, In the MSW handling area 20, trucks (not shown) are received and weighed by conventional means (not shown) . After an initial weight is taken, the truck unloads MSW into piles 48a and b. Preferably, the MSW does not need to be sorted and consists of biodegradable waste material. However, if the MSW comprises large amounts of nonbiodegradable material, such as appliances, automobiles and parts thereof, metal and the like, it may be sorted and such nonbiodegradable material removed. After unloading the MSW, the truck is again weighed to provide an accurate weight for the MSW unloaded. A front end loader 50 places the MSW 48 into one of the hopper assemblies 46a, b, c, or d. Turning now to Fig. 2, hopper assembly 46a comprises the following major elements: a funnel 54, a sliding bottom 56, ram housing 58, ram 60, ram piston 62, sliding bottom piston 64. Funnel 54 has an open top for receiving MSW and communicates with ram housing 58 through sliding bottom 56. Sliding bottom 56 has a closed positio. in which MSW can not enter ram housing 58. The sliding bottom 56 is maintained in a closed position to avoid MSW falling behind the ram 60 and to direct MSW into vessel 12. As best seen in Fig. 2A, sliding bottom 56 has a forward edge 66 which is tapered to cooperate with a notch 68 on the funnel 54. The interfitting edge 66 and notch 68 locks the sliding bottom 56 in a closed position, and stabilizes sliding bottom 56 from pressures exerted by MSW powered by ram 60 through ram housing 58. Sliding bottom 56 is coupled to a sliding bottom piston 64. Sliding bottom piston 64 powers sliding bottom 56 to allow sliding bottom 56 to assume an open position in which funnel 54 communicates with ram housing 58 and a closed position in which funnel 54 does not communicate with ram housing 58. Ram housing 58 communicates with vessel chamber 70, defined by the cylindrical wall 34 and ends 36a and 36b of vessel 12, by an opening 72. Opening 72 has a pivoting hatch 74 capable of assuming an open position and a closed position. Ram 60 is coupled to ram piston 67 to power MSW, entering ram housing 58 by gravity from funnel 54, through opening 72 into chamber 70. Ram piston 62 and sliding bottom piston 64 cooperates to maintain sliding bottom 56 in an appropriate position during the operation of ram 60. Preferably, ram piston 62 and ram 60 exert a pressure of 2,000 psi on MSW and can load approximately 70 cubic feet of MSW per minute at a rate of four strokes per minute. In the alternative, cylinder 56 is equipped with an auger [not shown] which upon rotation propels the refuse through an opening such as door 38. However, a preferred opening is located about the center of the end of vessel 12, to allow vessel 12 to be rotated during the loading operation. The chamber 70 of vessel 12 is preferably sizec to hold 230-270 metric tons of MSW, Vessels 12, 14, 16 and 18 communicate with sludge storage means 24, such as a tank or reservoir, to allow sludge to be pumped into each vessel. As best seen FIG. 1, sludge reservoir 24 is in fluid communication with vessels 12, 14, 16 and 18 through sludge conveying line 26. Sludge conveying lines 26 comprise an overhead manifold 80 and hoses 82 of which only one hose may be seen for each vessel 12, 14, 16 and 18. Each hose 82 has a quick connect fitting [not shown] which can be connected to a receiving fitting [not shown] on each vessel 12, 14, 16 and 18. Access to the fitting is made by operators by an inspection bridge 90. Alternatively, a catwalk [not shown] running the full length of the vessel can also be installed. Preferably, the in-ground reservoir 24 will hold at least one week's processing requirements. The sludge is placed in each vessel 12, 14, 16 and 18 while the vessel is stationary. Vessels 12, 14, 16 and 18 communicate with finished product conveying means 22. Turning now to Fig. 1, vessel 12 has an opening [not shown] equipped with a pivoting door 94. Door 94 has an open position and a closed position. In an open position, each vessel 12, 14, 16, and 18 empties into a hopper 96 which directs finished product or to suitable finished product conveying means 22, such as an endless belt, traveling cars or dumpsters and the like. Door 94 is controlled hydraulicly by hydraulic cylinder 94a. The finished product, a compost-like material transferred to a primary rotary trommel screening apparatus 98a and/or secondary rotary trommel screening apparatus 98B. Thereafter, the finished product is conveyed by conveying means 22 to storage areas lOOa-c for bagging as a high value fertilizer, or handled in bulk in storage areas lOOd-f, as suggested by front end loader 50. Vessels 12, 14, 16 and 18 are in fluid communication with output conduits 32. Output conduits 32 carry off gases generated in the processes or vent vessels 12, 14, 16 and 18. Output conduits 32 are in fluid communication with scrubber 28. Scrubber 28 removes noxious odors from such gases. Turning now to FIG. 4, vessel 12 is illustrated in cross section. Vessel 12 has a double-walled construction comprising an outer aluminum wall 110 and an inner carbon steel wall 112. Walls 110 and 112 are held a spaced distance apart by channel irons 114. A layer of thermal insulation 116 occupies space between walls 110 and 112 to facilitate temperature control through vessel 12. Typical dimensions of vessels 12, 14, 16 and 18 are an inner diameter of 14 feet 3/8 inches, inner wall 112 of 5/8 inch thickness, and outer wall 110 of 1/32 inch thickness, and an outer diameter of 16 feet. Mixing means comprises spikes 118 and stringers 120. Steel spikes 118 and stringers 120 project into the chamber 70 of vessel 12, from the wall 112. Stringer 120 is a 1/2-inch x 12-inch steel projection set at a 15° angle with respect to the vessel diameter and running the full iength of the vessel. Spikes 118 project radically inward from the wall 112. Spikes 118 have a typical size of 1/2 inch by 2 inches by 7 inches. Spikes 118 are located every two feet around the entire circumference inner wall of the vessel to form a ring of spikes. A ring of spikes is placed two feet longitudinally along the length of the vessel 12. Stringer 120 and spikes 118 tear and tumble solids within chamber 70 to create solids of smaller particle size. Vessel 12 is equipped with mixing means which may comprise rotable augers [not shown], paddles [not shown], and, most preferably, one or more baffles 122. Each baffle 122, illustrated in FIGS. 4 and 5, has two flat planar surfaces 124a and 124b, and a shaft 126. Shaft 126 protrudes through an opening in the vessel and is coupled to a linkage 128. Linkage 128 is coupled to an arm 130, as best seen in FIG. 2. Arm 130 connects a plurality of linkages 128 and baffles 122 for cooperating movement. In order to depict features of the vessel 12 with clarity, only two baffles 96 are illustrated in FIG. 4. The two baffles 122 form a ring of baffles at such point in the vessel 12. However, four or more baffles 122, arranged in a ring to substantially encircle the inner periphery of the vessel 12 are preferred. Baffles 122 are capable of rotation at shaft 101 to assume at least two of four positions. One of the four positions is a neutral position with respect to the rotation of the vessel. As best seen in FIG. 4, in this position the baffles 122 have flat planar surfaces 124a and 124b aligned with the plane of movement. In this position the baffles may cut through the solids and liquids contained in chamber 70, but do not impart movement to such solids and liquids. Turning now to Fig. 5, a second position is assumed by baffle 122 by rotation of baffle 122 at shaft 126 along arc C to incline the baffle 122 with respect to the plane of movement. Baffle 122 in such an inclined position urges solids and liquids toward one of the ends of the vessel, to facilitate loading and discharging material. This inclined position is preferably 30° from the plane of rotation. It is desirable to maintain the rotation of vessel 12 in one direction to conserve rotational momentum. A second position comprises inclining the baffle 122 in a second opposite inclined position, to urge the solids and liquids toward the opposite end of the vessel. With rotation of the vessel in one direction, baffle 122 allows movement of solids and liquids in two directions. Preferably, vessel 12 is equipped with sufficient baffles 122 to form a ring of baffles at points along the length of the vessel 12, which rings of baffles 122 are spaced such that the inclined position of a baffle 96 in one ring of baffles cooperates with a baffle 122 in a second ring, to form an auger-like configuration on the interior wall 64 of the vessel. Baffles 122 can be inclined to assume such an auger-like configuration or to act apart from each other to direct solids and liquids in a plurality of directions to effect mixing. A fourth position of the baffles 122 comprises baffles 122 assuming a position in which the flat planar surfaces 124a and 124b are perpendicular to the rotation movement of the vessel, to mix and tumble solids and liquids in the vessel without imparting significant movement toward either end of vessel 12. However, this position is not preferred due to the stress placed on shaft 126. Further, large rotational arcs of baffles 122 may interfer with stringers 120 and spikes 118. Input conduits 30 conveys air or oxygen, water, or inert quenching gases, such as carbon dioxide, into respective chambers 70 of vessels 12, 14, 16 and 18. Input conduits 30 comprises a nozzle injector 140, distributor 142 and aeration pipes 144a, b, c, and d, as best seen in FIGS. 3, 6 and 7. Distributor 142 is centrally affixed to one end of vessel 12. Preferably, distributor 142 is affixed by bolts to end 38b of vessel 12, opposite the end in which the vessel is loaded to allow the opening for receiving solid organic waste material to be positioned centrally. Turning now to FIG. 4, distributor 142 is in fluid communication with nozzle injector 140 and aeration pipes 144a-d. Aeration pipes 144a-d extend radically from the distributor 142, to the cylindrical wall 112. The aeration pipes 44a-d continue axially the length of cylindrical wall 112, as best seen in Fig. 3. The aeration pipes 144a-d have openings 146 for venting gases into chamber 70. Preferably, aeration pipes 144a-d are positioned adjacent stringers 120, to allow the stringers to protect the aeration pipes 144a-d during the rotation of vessel 12. Distributor 140 has an interior cavity 150 with a valve plate 152. Valve plate 152 has a stationary opening 154 which allows gases to flow from nozzle injector 140 to aeration pipes 144a-d. Valve plate 152 closes the flow of gases to aeration pipes 144a-d as such pipes are assuming a position at the bottom of the rotation of vessel 12, and open the gas flow to aeration pipes 144a-d as such pipes assume a position at the top of the rotation of vessel 12. Thus, turbulence within the admixtures, normally contained within 85% of the said volume of the vessel 12, is minimal. Air flow is maintained in the upper 15% of the said space of the vessel 12. Input conduit 30 is in communication with a plenum 202 positioned distally from vessels 12, 14, 16 and 18, as best seen in FIG. 8. Plenum 202 combines and mixes gases for entry into chamber 70 of vessel 12. Plenum 202 is in communication with a source of air. Preferably, the air is filtered by electrostatic filtering unit 206 and heated by hot water heat exchanger 208, if necessary. Hot water heat exchanger 208 is in communication with a hot water boiler 212, of conventional design, by water line 266a. A circulator 266b pumps fluid through hot water boiler 212 and water line 266a. A shunt 266c carries water to exchanger 208. Flow through shunt 266c is controlled by valve 256. The plenum 202 is in communication with a source of an inert gas, such as carbon dioxide through mixing manifold 216. As used herein, an inert gas is a gas which does not participate in the biological process to a significant degree and can be used to adjust the metabolic processes in vessel 12. Carbon dioxide, the by-product of the metabolic processes within vessel 12, does not significantly participate in further processes other than influence buffering and pH levels of liquids within the vessel 12. Carbon dioxide enters plenum 202 through mixing manifold 216 through injection nozzles 218 and 220. Plenum 202 is in communication with a source of water. Water is processed by atomizing humidifier 214 to enter plenum 202 as a vapor. Atomizing humidifier 214 is controlled by humidifier controller 251. Preferably, plenum 202 receives gases and water in response to a computer processing unit 200. As shown in FIG. 8, a computer processing unit 200 (CPU) receives signals from vessel sensors for carbon dioxide 234, water 236, temperature 238, oxygen 232, and methane 238. Input conduits 30 have sensors to monitor the conditions of gases entering vessels 12, 14, 16 and 18. These sensors comprise temperature sensing element 222, moisture 224, and carbon dioxide sensing element 226 placed on the output side of the plenum 202 to monitor the air mixture. Input conduits have one or more blowers 228 to propel gases into vessels 12, 14, 16 and 18. The flow rate of air 204 into the plenum is determined by the speed of each blower 228 as controlled by the CPU 200. The CPU 200 is connected by coaxial fiber optic cable 240 to the analog-digital encoder 242. The carbon dioxide sensor 230 is connected by leads 244 to the manifold 216 and simultaneously is connected by leads 246 to encoder 242. The manifold 216 is connected by leads 253 to encoder 242. The oxygen sensor 232 is connected by leads 248 to the encoder 242. The moisture sensor 234 is connected by leads 250 to the humidifier controller 251 which is also connected by leads 252 to the encoder 242. The temperature sensor 236 is connected by leads 254 to the diverting zone valve 256 which is connected by leads 258 to the encoder 242. Methane sensor 238 is connected by leads 260 to the encoder. Encoder 242 is connected by leads 262 to boiler controller 212, and the encoder is also connected by leads 264 to circulator pump 266. Encoder 242 is connected by lead 268 to sensor 222, by lead 270 to sensor 224, by lead 272 to sensor 226. The construction of CPU 200 is conventional and could be similar to those structures as shown in the Larson U.S. Patent No. 3,178,267 or shown in the Yeagley U.S. Patent No. 4,499,614. The disclosure of these patents is herewith incorporated by reference. In response to signals from sensors 230-238, CPU control valves for water, air, carbon dioxide and the temperature of gases entering plenum 202. Within plenum 202, air, water, carbon dioxide and temperature are combined to generate the conditions required by the multi-flora microbial population inside the rotating vessels 12, 14, 16 and 18. The CPU controls the conditions within the mixing plenum 202 such that the preconditioned air has a temperature of about 98.6° F, such that the moisture content of the gas mixture is 33% by volume, the carbon dioxide content of the gas mixture is up to 25% by volume, and the balance, or 42% by volume, is air. Conduit 74 delivers from 320 to 350 ft. 3 /min. of this preconditioned gas mixture into one or more of vessels 12, 14, 16 and 18. For example, temperature sensor 236 may signal that the temperature in vessel 12 is above or below the required or reference temperature for vessel 12. CPU 200 will actuate encoder 242 to send a signal to boiler controller 212, and to circulator 266 and to valve 256 to adjust the water temperature and flow rate into heat exchanger 208 in order to affect the appropriate temperature correction by adjusting the water flow rate, By way of example, moisture sensor 234 may signal that the humidity in vessel 12 is above or below the required or reference moisture content for vessel 12. CPU 200 will actuate encoder 242 to send a signal to humidifier controller 251 in order to affect the appropriate humidity correction by adjusting the moisture flow rate through humidifier 214. By way of example, the presence of methane within vessel 12 may indicate a lack of adequate air flow into the vessel. Upon detecting methane via methane sensor 238, the CPU 200 through encoder 242 may cause blower 228 to increase the flow rate of air to enter vessel 12 through input conduit 30 by sending a signal over lines 280. CPU 200 may make adjustments in temperature, moisture, and oxygen content to impose first, second or third growth conditions throughout the entire vessel. First growth- conditions comprise a temperature of 165° to 200°F, gaseous water concentration of gases within the vessel of 25 to 40%, and an oxygen gas concentration to promote the growth of thermophilic microorganisms. Second growth conditions comprise a temperature of 145° to 164°F, a gaseous water concentration of 25-45%, and an oxygen concentration sufficient to promote the growth of mesophilic microorganisms. Third growth conditions comprise a temperature of 110° to 144°F, gaseous water concentration on 25 to 45% and sufficient oxygen concentration to promote the growth of actinomycetes, protozoa and fungi. Thermophilic and mesophilic microorganisms and actinomycetes, protozoa and fungi may be maintained in storage vessels (not shown) if cultures of cell organisms are desired. In operation, with respect to one vessel 12, solid organic waste material and sludge are loaded into vessel 12 to occupy 85% of the void volume of the vessel. Vessel 12 is filled with a solid organic waste material and sludge to form an admixture having a weight ratio of carbon to nitrogen of 25-32:1. A preferred carbon-to-nitrogen weight ratio is 30:1. The vessel is rotated and baffles 96 are inclined to distribute the material throughout the vessel. The vessel 12 is rotated with the stringers 70 and spikes 72 tearing and tumbling the solid organic waste material and sludge. These tearings and tumblings create a large surface area and cause billions of bacteria in a multi-microbial flora, to start the biodegradation of all organic matter present in the refuse and sludge. Chamber 70 of vessel 12 is brought to first growth conditions on the first day to promote digestion of the admixture of solid organic waste material by the thermophilic bacteria to form a thermophilic biodegradation product. The rotation of the vessel will continue for 24 to 36 hours, as gases, comprising air, oxygen and water are placed in the vessel 12 to create growth conditions for thermophilic bacteria. Such gases are preconditioned in mixing plenum 202 located outside of the vessel. The entire chamber 70 of vessel 12 is brought to a second set of growth conditions on the second day to promote digestion of the thermophilic biodegradation product by mesophilic bacteria to create a mesophilic biodegradation product. In the event insufficient mesophilic bacteria remain after degradation by thermophilic bacteria, an admixture is made of a mesophilic bacterial culture and the thermophilic biodegradation product. The mesophilic culture may contain any number of mesophilic bacteria, and preferably comprises bacillus subtillis. The entire chamber 70 of vessel 12 is brought to a third set of growth conditions on the third day to promote digestion by combination of aerobic microorganism comprising actinomycetes, protozoa and fungi. In the event insufficient aerobic microorganisms remain after digestion by thermophilic bacteria, an admixture is made of a culture of such aerobic microorganisms and the mesophilic biodegradation product. This culture may contain any number of microorganisms and preferably comprises actinomycetes. Microorganism comprising cultures are preferably selected for similar growth profiles. As each of the growth conditions are imposed, the vessel rotates to provide mixing and temperature uniformity, During the approximately first 24 hours, the thermophilic growth conditions promote reproduction and digestion of the organic material by the thermophilic bacteria. Digestion of the MSW and sludge by the thermophilic bacteria causes the temperature to rise to about 175° F to 178° F. Following the initial elevated temperature, the temperature is slowly decreased from 175° F to 120° F. The thermophilic bacteria stops reproducing. This temperature is controlled by air flow at a lower temperature at 98.6° F. The computer processing unit 200 controls the process variables within the vessel 12. Preferably, the temperature ranges from 175° F to 178° F, the moisture content of the air is 33% by volume, the carbon dioxide content of the air is 25% by volume, and sufficient oxygen is present to support growth of thermophilic organisms. During the imposition of first growth conditions, a thermophilic biodegradation product is formed. During the second 24-hour interval, a second set of growth conditions are imposed throughout the entire vessel 12. The thermophilic biodegradation product formed during the first growth conditions is subjected to growth conditions favoring mesophilic microorganisms. In the event insufficient mesophilic microorganisms survive the thermophilic growth conditions, an inoculum of mesophilic organisms, from a stored culture [not shown] , is placed in vessel 12 through openings which normally receive hoses 44. A second admixture of mesophilic microorganisms and the thermophilic biodegradation product is formed. The mesophilic bacteria thrive and reproduce at a temperature range of 145° F to 162° F. Air and moisture are maintained to provide sufficient oxygen for biological processes. After 24 hours, the temperature of the admixture of mesophilic microorganisms and the thermophilic biodegradation product is lowered by flushing the vessel 12 with cooler air to end the mesophilic growth conditions. The mesophilic microorganisms have, during this period biodegraded the thermophilic biodegradation product to form a mesophilic growth product. Preferably, during the mesophilic growth conditions, the temperature ranges from 145° F to 162° F, the moisture content of the air is 30% by volume, the carbon dioxide content of the air is 23% by volume, and oxygen is present in sufficient concentration to promote growth of mesophilic organisms. Preferably, these parameters are controlled by a computer processing unit 200. During the third 24-hour interval, a third set of growth conditions are imposed throughout the entire vessel 12. The mesophilic biodegradation product formed during the second growth conditions is subjected to growth conditions favoring microorganisms comprising actinomycetes, protozoa and fungi. In the event insufficient actinomycetes, protozoa and fungi survive, an inoculum of such organisms, from a stored culture [not shown] is placed in vessel 12 through openings which normally receive hoses 44. A third admixture of a microorganism comprising actinomycetes, protozoa and fungi is formed. Third grown conditions comprise a temperature range from 120° F to 144° F, a water content of the air at 27% by volume, and sufficient oxygen to promote growth. Growth is monitored by examining the carbon dioxide content of the air. Preferably, the carbon dioxide content is maintained at 19% by volume. At the completion of the third growth conditions, the initial starting materials have been reduced to a compost-like organic material suitable for agricultural purposes, including as a fertilizer. Upon completion of the third 24 hour period, the temperature drops to approximately 110° F. Preferably, the computer processing unit 200 controls the process variables. Preferably, the computer process unit 200 will stop the vessel's rotation, activate the hydraulic discharge gate-valves 96 at its output end 38b, as shown in FIG. 1, and move the variable pitch baffles 122 in the rotating vessel 12 from the neutral position shown in FIG. 4 to a 30° forward pitch, as shown in FIG. 3. The finished compost will begin to discharge into the hoppers 96a, and then from these hoppers onto the conveyor means 22. The conveyor means 22 will commence a forward motion, to the right, as shown in FIG. 1, toward the primary rotary trommel screening device 98 The system is flexible enough to accommodate both manual and fully automated sorting and separation. Preferably, the plant will be fully automated by incorporating a ferrous metal separator unit [not shown] and another nonrecyclables separator unit [not shown] next to the rotary trommel screening device 98a. The screened tailings of the primary trommel unit 98 can be safely carted away to a landfill, since it has been exposed to reasonably high temperatures for a number of days. For all practical purposes, it can be said that they were "autoclaved" during the first growth conditions. The same applies to rejected material in the sorting and separation process, most of which is ready for recycling, and is free from contaminants and pathogenic bacteria. The end organic material product is a fine compost or humus or soil additive with specifications that meet and exceed EPA compost Type 1 standards for agricultural use. The end product results from having the bacteria convert the organic carbon in the MSW, and the nitrogen in the sludge into protein. The product quality control can be closely monitored by a biotechnology professional in a plant site lab equipped to handle necessary testing. While several embodiments of the present invention have been shown and described, it is to be understood that many changes and modifications may be made thereunto without departing from the spirit and scope of the invention as defined in the appended claims.

Claims: CLAIMS 1. A method of making an organic material from solid organic waste material and sludge comprising: a. forming an admixture of a solid organic waste material and sludge in a containment means, said containment means comprising one or more vessels having mixing means, gas input means, water input means, temperature control means, gas output means, and opening means, said opening means for receiving solid organic waste material and sludge and discharging one or more biodegradable products, said mixing means for maintaining said admixture in contact with gases and water and to provide temperature uniformity within said vessel, said gas input means, water input means, and temperature control means for imposing one or more growth conditions within said one or more vessels, said gaseous output means for removing gases from said one or more vessels; b. imposing first growth conditions on said admixture, said first growth conditions comprising a temperature of 165° to 200°F, gaseous water concentration of gases within the vessel of 25 to 40%, and an oxygen gas concentration to promote the growth of thermophilic microorganisms in said admixture, said thermophilic microorganisms biodegrading said admixture to form a thermophilic biodegradation product; and c. in the event said thermophilic biodegradation product contains insufficient mesophilic microorganisms, forming a second admixture comprising a mesophilic microorganism and said thermophilic biodegradation product and imposing second growth conditions on said second admixture or said thermophilic biodegradation product, said second growth conditions comprising a temperature of 145° to 164°F, a gaseous water concentration within said vessel of 25 to 45%, and an oxygen gas concentration sufficient to promote the growth of one or more mesophilic microorganisms, said mesophilic microorganisms biodegrading said thermophilic biodegradation product to form a mesophilic biodegradation product comprising an organic material. 2. The method of claim 1 further comprising the step of forming a third admixture in the event said mesophilic biodegradation product contains insufficient microorganisms from a third microorganism group, said third admixture comprising said mesophilic biodegradation product and a third microorganism group comprising actinomycetes, and imposing third growth conditions on said third admixture or said mesophilic biodegradation product, said third growth conditions comprising a temperature of 110 to 144°F, gaseous water concentration with the vessel of 25 to 45%, and sufficient oxygen gas concentration to promote the growth of said one or more actinomycetes, said actinomycetes biodegrading said mesophilic biodegradation product to form an organic product. 3. The method of claim l wherein said organic product is a compost for agricultural applications. 4. The method of claim 1 wherein said admixture of a solid organic waste material and sludge has a pathogen load, and said first growth conditions, are incompatible with said pathogens to form a thermophilic biodegradation product with a reduced pathogen load. 5. The method of claim 1 wherein said temperature and said oxygen and said water concentration are maintained by the flow of gases through said vessel, through gas inlet means and gas outlet means, 6. The method of claim 1 wherein said temperature is controlled by reducing the flow of gases to produce higher temperatures, and increasing said flow to reduce said temperature. 7. The method of claim 1 wherein said gases used to reduce said temperature is a gas which is substantially inert in the biological process. 8. The method of claim 7 wherein said gas is carbon dioxide. 9. The method of claim 1 wherein said gas used to produce a temperature of 165° to 200°F is oxygen, to promote growth by microorganisms. 10. The method of claim 1 wherein said gases are mixed in a plenum in fluid communication with said vessel inlet. 11. The method of claim 1 wherein said outlet is in communication with a scrubber to remove noxious odors. 12. The method of claim 11 wherein said scrubber imposes removal conditions, to remove noxious gases during a period in which thermophilic growth conditions are imposed. 13. The method of claim 12 wherein said removal conditions are imposed during a two hour period beginning with the imposition of thermophilic growth conditions. 14. The method of claim 1 wherein said thermophilic microorganisms are present in the sludge. 15. The method of claim 1 wherein said mesophilic microorganisms comprises Bacillus subtillis. 16. The method of claim 13 wherein vessel mixing means comprise means for rotating said vessel. 17. The method of claim 16 wherein said vessel has one or more baffles having planar surfaces extending inward from the cylindrical wall into said chamber for imparting direction and movement to solids and liquids to facilitate mixing. 18. The method of claim 17 wherein said one or more baffles are rotatable to assume at least two of four positions, said four positions comprising a first inclined position with respect to the vessel rotation wherein said planar surfaces move solids and liquids in a first direction, a second inclined position with respect to the vessel rotation wherein said planar surface move solids and liquids in a second direction opposite said first direction, a third position wherein said planar surfaces are perpendicular to the vessel rotation to maintain said solids and liquids in an area of said vessel while subjecting said solids and liquids to mixing, and a fourth position wherein said planar surfaces and the plane defined by the rotation of the vessel at said baffles are approximately equal to allow rotation of the vessel with minimal mixing. 19. The method of claim 18 wherein said vessel has a plurality of baffles which baffles assume one of said four positions in cooperation to provide movement of solids and liquids. 20. The method of claim 19 wherein said plurality of baffles form an auger-like spiral about said cylindrical wall of said vessel . 21. The methods of claim l wherein said vessel comprises shredding means for tearing solids as said vessel is rotated. 22. The method of claim 21 wherein said shredding means comprises inwardly projecting spikes. 23. The method of claim 1 wherein said vessel is an elongated cylinder with two ends, one of said ends having a first opening means for receiving solid organic waste material and said opposite end having second opening means for discharging one or more organic products. 24. The method of claim 1 wherein said vessel has sensors for monitoring conditions for microorganism growth selected from one or more of the parameters comprising temperature, water, carbon dioxide and oxygen. 25. The method of claim 24 wherein said sensors are in communication with computer monitoring means. 26. The method of claim 1 wherein said first growth conditions comprise a temperature range of 175° to 178°F. 27. The method of claim 1 wherein said second growth conditions comprise a temperature range of 145° to 162°F. 28. The method of claim 1 wherein said third growth conditions comprise a temperature range of 120° to 144°F. 29. An apparatus for processing solid organic waste material and sludge comprising: a. a vessel having a cylindrical wall having an axis and two opposing end walls, which cylindrical wall and end walls define a chamber, said vessel having opening means, mixing means, gas input means, water input means, temperature control means, and gas output means, said opening means for receiving solid organ waste material and sludge, and discharging one or more biodegradation products; said mixing means for forming one or more admixtures of solid organic waste material, sludge, biodegradation products and microorganisms, for bringing said one or more admixtures in contact with gases and water and to provide temperature uniformity throughout said vessel, said mixing means cooperating with the rotation of said vessel to distribute solids and liquids throughout said vessel upon receiving solids and liquids within said chamber from opening means and to propel said solids and liquids to said opening means to discharge said solids and liquids from said vessel; said gas input means, water input means, and temperature control means for imposing one or more growth conditions within said vessels, said gas output means for discharging gases from said vessel; and vessel rotating means for rotating said vessel about said axis in cooperation with said mixing means to direct movement of said solids within said vessel; said vessel for receiving solid organic waste material and sludge within said chamber, said mixing means forming a first admixture of said solid organic waste material and sludge, and said vessel imposing first growth conditions, said first growth conditions comprising a temperature of 165 to 200°F, gaseous water in a concentration of 25 to 40%, and sufficient oxygen to promote growth of thermophilic microorganisms, said thermophilic microorganism biodegrading said first admixture to form a thermophilic biodegradation product, and said vessel for receiving a mesophilic microorganism through said opening means if said mesophilic microorganism is not present in sufficient amounts in said thermophilic biodegradation product and said mixing means forming a second admixture comprising said thermophilic biodegradation product and said mesophilic microorganism, said vessel for imposing second growth conditions on said second admixture or said thermophilic growth to promote growth of said mesophilic microorganisms, said second growth conditions comprising a temperature of 145° to 164°F, gaseous water of 25 to 45%, and sufficient oxygen to support growth of mesophilic microorganisms to form a mesophilic biodegradation product comprising an organic material which is discharged from said chamber by mixing means. 30. The apparatus of claim 29 wherein said vessel receives a third microorganism group if said third microorganism group is not present in sufficient amounts in said mesophilic biodegradation product, comprising actinomycetes, said mixing means forming a third admixture comprising said third microorganism group and said mesophilic biodegradation product, said vessel imposing third growth conditions on said third admixture or said mesophilic biodegradation product, said third growth conditions comprising a temperature of 110° to 144°F, a gaseous water concentration of 25 to 45%, and sufficient oxygen to support the growth of one or more actinomycetes for forming a third biodegradation product comprising an organic material. 31. The apparatus of claim 29 further comprising a scrubber in communication with said gas output means to remove noxious gases, 32. The apparatus of claim 29 wherein said vessel comprises sensors for one or more of the following compositions comprising carbon dioxide, water, methane and oxygen, and one or more sensors for temperature. 33. The apparatus of claim 32 wherein said one or more sensors are in communication with computer control means for regulating gas input means, water input means and temperature control means , 34. The apparatus of claim 29 wherein said mixing means comprises one or more baffles projecting inwardly into said chamber from said cylindrical wall, said baffles having a planar surface for imparting movement and direction to solids and liquids, said one or more baffles capable of assuming at least two of four positions, one of said positions comprising said planar surface inclined for directing solids and liquids in a first direction upon rotation of said vessel, one of said positions comprising said planar surface inclined for directing solids and liquids in a second direction opposite said first direction upon rotation of said vessel; one of said positions comprising said planar surface perpendicular to the axis of rotation to mix solids and liquids without imparting movement of solids and liquids to one of said ends for mixing said solids and liquids, and one of said positions comprising said planar surface in a plane defined by the arc of rotation of said vessel, which allows rotation of said vessel without substantial mixing. 35. The apparatus of claim 29 wherein said vessel rotating means comprises rollers. 36. The apparatus of claim 35 wherein said vessel comprises tracks for receiving said rollers for maintaining the position of said vessel on said rollers. 37. The apparatus of claim 34 wherein said mixing means further comprise stringers.

Inventors: ARRAU AGUSTIN H, ARRAU, AGUSTIN, H.
Applicants: ARRAU AGUSTIN H, ARRAU, AGUSTIN, H.
Application year: 1994
Main classification: B01J8
IPC codes: C05F15, C05F17